US3498378A - Oil recovery from fractured matrix reservoirs - Google Patents

Oil recovery from fractured matrix reservoirs Download PDF

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US3498378A
US3498378A US3498378DA US3498378A US 3498378 A US3498378 A US 3498378A US 3498378D A US3498378D A US 3498378DA US 3498378 A US3498378 A US 3498378A
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oil
matrix
water
pressure
production
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Herbert L Stone
John W Graham
Robert J Blackwell
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ExxonMobil Upstream Research Co
Esso Products Research Co
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ExxonMobil Upstream Research Co
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    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16Enhanced recovery methods for obtaining hydrocarbons
    • E21B43/18Repressuring or vacuum methods
    • EFIXED CONSTRUCTIONS
    • E21EARTH DRILLING; MINING
    • E21BEARTH DRILLING, e.g. DEEP DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
    • E21B43/00Methods or apparatus for obtaining oil, gas, water, soluble or meltable materials or a slurry of minerals from wells
    • E21B43/16Enhanced recovery methods for obtaining hydrocarbons
    • E21B43/20Displacing by water

Description

ocmw!! MINE?! H. L. STONE ET AL March 3, 1970 3,498,378

OIL RECOVERY FROM FRACTURED MATRIX RESERVOIRS Filed June 9. 1967 NOllVHnlVS GII'TH m .v m

O ON

Herberl LA Stone INVENTORS Robert J. Blackwell ATTORNEY United States Patent O U.S. Cl. 166-263 6 Claims ABSTRACT OF THE DISCLOSURE A method for recovering oil from fractured matrix reservoirs using cyclic pressure wateroodingand rendering the surface of the rock ntrix oil-wet prior to the production phase.

BACKGROUND OF THE INVENTION This invention pertains to a process for inserting a fluid into the pores of the formation -by means of a shaft or deep boring in the earth commonly known as a well.

SUMMARY Many reservoirs from which oil and gas are produced :are relatively homogeneous with respect to porosity and permeability of the formation. However, it is recognized that a large number of producing formations, especially the carbonate rocks, are naturally and highly fractured. A typical example of such a reservoir is the S'praberry trend of West Texas.

Highly fractured reservoirs consist of two distinct elements, fractures and matrix, each having its characteristic porosity and permeability. The oil-bearing porous rock matrix is interlaced by an extensive network of naturally occurring fractures or fracture-like channels characterized by fluid conductivities which may exceed the matrix permeability by a factor of several thousand. Experience has proven that the recovery of oil from such reservoirs by normal production practices is far less ellicient than from unfractured reservoirs having generally the same matrix character and initial fluid saturations. During the primary production, the natural reservoir pressure is rapidly depleted through the highly conductive fracture system, typically leaving more than 90% of the original crude saturation in place. In essentially the same manner, conventional methods of secondary recovery have failed to displacesubstantial volumes of oil.

Conventional Waterflooding techniques are relatively ineffectual in highly fractured reservoirs. The floodwater tends to flow through the interconnected fissures, grossly bypassing the oil which is in the matrix. As a result, only that oil which is left in the fractures following primary production is recovered in conventional waterflooding. Watertlooding in these reservoirs in characterized 4by early water break-.through and rapidly reached uneconomic producing water-oil ratios.

One modification of the conventional waterilooding process which has achieved limited success is countercurrent imbibition. In a fractured reservoir, if the rock surfaces of a matrix system are sufliciently water wet, limited recovery by this method is possible. Water is injected into the fractures and allowed to remain in contact with the rock matrix for a period of time ranging from weeks to several years. During this contact period water is spontaneously imbibed ino the matrix and there is a countercurrent explusion of oil into the fracture system. The expelled oil is swept through the fractured system to production wells where it is recovered in the conventional manner. Waterllood recovery by countercurrent ice imbibition maybe further improved by the use of surface active agents which reduce interfacial surface tension between the oil and water phase as disclosed in US. Patent 2,792,894. The effect of such surfactants is to further increase the -water wettability of the rock matrix and/or to reduce the interfacial tension 'between the oil and water phases and thereby increase the ability of the rock to imbibe water and increase the oil expulsion. ln a countercurrent imbibition process, with or without the addition of a water-wetting surfactant,` the rate of oil recovery is dependent upon the capillary pressure char acteristics of the porous rock matrix. Tlfats, the imbibition process is essentially'unatfected by conventional techniques for controlling eld operations, such as selecting pressures and flow rates.

Another modification of the waterllooding process as applied to fractured reservoirs is known as cyclic pressure flooding or pressure pulse flooding. Cyclic pressure flooding is accomplished by alternately increasing and decreasing the net production and injection rates which thereby create a cyclic pressure differential between the rockvmatrix and the fracture system. The pressure pulse process does not rely primarily upon imbibition to displace resorvoir oil. Instead, the cyclic variations in pres-l sure force water in to the' rock matrix and oil from the matrix into the fractures. l

In the initial phase of cyclic pressure flooding, net fluid production is limited toa rate substantially below the volumetric water influx, lwhereby the reservoir pressure is raised to a high`level. This phase of the cycle is known as the injection phase, during which little or no oil is produced; The pressure buildup in the fracture system forces ya portion of the injected water to enter the porous matrix.v

,After a period of time sullicient to permit a substantial approach toward pressure equilibrium between the fracture system and the porous matrix, the production phase of the cycle is begun. Continued water injection is limited to a rate substantially below the net fluid production rate in order to reduce the reservoir pressure. Consequently, the pressure diEerence between the fracture system and the matrix blocks is reversed, thereby forcing oil from the pore system into the fracture system, where it is swept toward the production wells and recovered in a convenQ tional manner, l

Pressure pulse flooding has severalldistinct advantages over the countercurrent imbibition process. First, during' the injection cycle, all wells are available for injection of reservoir fluid, giving a more rapid increase in reservoir pressure. Second, because increased injection pressures and rates are used, the influx of the oodwater into the rock matrix is accomplished more rapidly. Third, due to the increased pressure, more gas is redissolved into the oil which provides energy for oil displacement during the production phase. Fourth, all wells into the reservoir are available for production duringr the production phase, thereby increasing the production rate.

Although the cyclic pressure method docs recover oil more rapidly, the amount of oil produced has proven to be about the same as produced in accordance with the imbibition process. It has been suggested, therefore, that oil production in the cyclic pressure process must be indirectly governed by essentially the same capillary forces as control the imbibition process.

The action of capillary forces during the cyclic pres=1 sure process tends to distribute oil and water saturations uniformly throughout each matrix block, regardless of the nature of inherent wettability characteristics of the rock. A uniform distribution of oil, however, is undesins able since the only producible oil isfthat located a relan tively short distance from a fracture channel. The cyclic pressure method can recover substantially increased volumes of oil 'if the capillary characteristics of the porous matrix system are modified such that equilibrium oil saturations in the matrix near the fracture system exceed the averageoil saturation.

Accordingly, it is an object of the present invention to improve the cyclic pressure waterooding method of petroleum recovery from fractured reservoirs by establishing a favorable gradient of fluid saturations in the matrix pore system. More particularly, it is an object of the invention to modify the capillary imbibition characteristics of the porous matrix such'that equilibrium oil saturations in the matrix near the fracture system exceed the average oil saturation prior to a production phase of the flood cycle.

These and other objects of the invention are accomplished by the addition of avsuitable chemical to the injected lloodwater at some time preceding the production phase of a waterflood cycle. Preferably, one or more such chemicals is added during the injection or repressuring phase of the first watertlood cycle. To the extent feasible, it is preferred to render the matrix face permanently oilwet, whereby the addition of chemicals during subsequent waterflood cycles becomes unnecessary.

It is known that a large class of surfactants have the ability to increase the wettability of a rock matrix with respect to either oil or water. One end of the surfactant molecule is preferentially adsorbed on the surface of the rock matrix. The opposite end of the surfactant molecule will preferentially attract water if it is a water-wetting surfactant, or oil if it is an oil-wetting surfactant. Whether the rock matrix is rendered oil-wet or water-wet by a given surfactant depends on the physical chemistry of that surfactant as is well known to those skilled in the art.

The surface active agents employed in the practice of the present invention may be selected from a large group of surface active agents which cause preferential wetting of the earth solids, such as sand, clay, shale, lime, quartz, dolomite, and the like, with hydrocarbons which may be present therein. The earth or rock solids priorto the contacting operation are preferentially wet by the water in the rock solids. After the contacting operation the earth or rock solids are preferentially wet by the hydrocarbons.

Among the surface active agents which are valuable and operable in the present invention may be mentioned the amine salts, the ammonium salts, and many others of a similar type. Specifically, the cationic salts are valuable and useful in the present invention. Exemplary of the compounds which have been found suitable in preferentially wetting rock solids by the hydrocarbons contained therein may be mentioned octadecyl amine acetate; cetyl dimethyl amine acetate; Tetrosan, a cationic surface active agent solid by Onyx Oil & Chemical Company, Jersey City, NJ.; the acetate of Primene JM-T, which is a mixture of primary amines with branched chains containing from l5 to 20 carbon atoms, sold by Rohm & Haas; Arquad 2-C which is dicoco dimethyl. ammonium chloride prepared from coconut oil; the amine acetate prepared from Primene 81-R, which is a mixture of primary amines containing branched chains of 12 to 15 carbon atoms, sold by Rohm & Haas; alkyl tolylmethyl trimethyl ammonium chloride; alkyl dimethyl benzyl ammonium chloride; lauryl benzyl dimethyl ammonium chloride; bis quaternary salts such as reaction products of 2-octyl benzyl chloride with bis dimethyl amino butyne and nonyl benzyl chloride with bis dimethyl amino butene; di-isobutyl cresoxyethyl dimethyl benzyl ammonium chloride and di-isobutyl phenoxyethoxy ethyl dimethyl benzyl ammonium chloride; and the like.

Suitable concentrations of the surfactant range from 0.05% up to as much as 5% by weight the upper limit being governed more by economics than technical feasi bility. It is preferred to inject water containing from 0.2% up to about 2.0% by weight surfactant. The volume of surfactant-containing water injected should at least be sufficient to contact substantially all matrix faces through the fracture system. The upper limit on injected volume is governed primarily by pressure requirements of the flood and under most operating conditions the maximum botn tom-hole pressure will be limited to the initial bottomm hole pressure of the reservoir.,

The surfactant is strongly and preferentially adsorbed on the rock matrix, and, upon contact with the matrix, the surfactant will concentrate near the surface of the block. The depth of invasion of the surfactant will normal ly range from a few inches to a foot or more. The depth of invasion for given operating conditions can be readily determined in the laboratory using techniques which are well known to those skilled in the art. It should be noted that although the surfactant is primarily located very near the surface of the matrix block, appreciable quantities of oil will be concentrated in this zone due to the large sur= face area of the matrix blocks.

Once a portion of the rock matrix adjacent the frac= ture system is rendered oil-wet, capillary forces cause the oil to accumulate preferentially in the oil-wet zone, andi water to accumulate preferentially in the water-wet zone, Therefore, during a subsequent production phase of the watertlood cycle, the oil which has accumulated near the matrix face is readily displaced into the fracture system.

DESCRIPTION OF THE DRAWINGS The practice of the invention can be more clearly seen with reference to the drawings:

FIGURE l is sectional view of two grains of the rock matrix in a water-wet system.

FIGURE 2 is a plot of capillary pressure versus iiuid saturation in a water-wet core of the rock matrix.

FIGURE 3 is a plot of the capillary pressure versus iiuid saturation in the same core as FIGURE 2 but which has been rendered oil-wet by the addition of a suitable surfactant.

FIGURE 4 s a plot of fluid saturation versus depth in. the rock matrix of a water-wet system subsequent to the injection phase but prior to the production phase of the cyclic pressure process.

FIGURE 5 is a plot of fluid saturation versus depth in the rock matrix subsequent to the injection phase and inversion of the wettability of the surface of the roclr` matrix.

DETAILED DESCRIPTION As was noted hereinbefore, capillary pressure is the force which governs4 the fluid distribution within the rock .matrix in the practice of this invention. The practice of this invention can be most clearly explained by describd ing the relationships between capillary pressures, fluid saturations and wettability characteristics of the rock matrix.

The capillary pressure between two fluids in a porous medium is a measure of a variety of physical character= Pc: the capillary pressure between the oil and water P0=the oil phase pressure at the interface Pw=the water phase pressure at the interface.,

In a water-wet system, the capillary pressure varies inversely with the water saturation. Two grains of the rock matrix of such a system with the wetting and. non-wetting fluids are seen in FIGURE l. Two grains It and 2 are surrounded by oil 3 as a non-wetting phase and hold between them water 4 as the wetting phase. At a high water saturation, the interface between the wetting and nonwetting phases will assume the-configuration shown at 5. But as the water saturation decreases, the interface withdraws to the position shown in 6. It can be seen that, as the water phase decreases in saturation, the curvature of the interface increases, thereby increasing the capillary pressure between the wetting and nonwetting phases.

FIGURES 2 and 3 show the relationship between capillary pressure and fluid saturation for a water-wet system and a'n oil-wet system, respectively. Referring to FIG- URE 2, it is seen that as the water saturation increases, the capillary pressure decreases along the trace shown by curve 7. In the water-wet system illustrated in FIG- URE 2, the capillary pressure always has a positive value; that is, the pressure in the oil phase is always greater than the pressure in the water phase. The driving force tending to distribute the fluids within the rock matrix is the difference in capillary pressure between any two given poi-nts in the matrix.

In arock matrix into which water is being injected, the water saturation at the interior of the rock matrix will be at an initial low level,V SW1, having a corresponding capillary pressure P61. Atvthe face of the fracture, the water saturation is relatively high, SW2, having the corresponding capillary pressure Pez. The force available to distribute the fluids withinthe reservoir rock is the difference in capillary pressures, Pci-Pc3.

In FIGURE 3` the corresponding capillary pressurefluid saturation relationship is shown for an oil-wet systern having the same geometric configuration of pore spaces as the -wet system in FIGURE 1. In this system, Pc is nve; that, is, `the pressure in the water phase always ex ds the pressure in the oil phase. l

Considering both FIGURES 2 andy 3, it can vbe seen that by inverting the wettability of the face of the rock; that is, changing the surface of the .rock matrixl from a water-wet system to an oil-wet system, the driving force available to expeloil .fronr'the center of the rock matrix to its face has been increased from Pci-Peg to Bev-Pcs. This effect would tend to concentrate the oil in the wetting phase at the surface of the rock matrix prior to the production phase.

FIGURES 4 and 5 are a compartive illustration of the fluid saturations within the matrix for a water-wet system having its wettability inverted at the face of the rock matrix. FIGURE 4 shows the uid distribution in the rock matrix subsequent to the injection phase but prior to the production phase of the cyclic presstre process. At the interior of the matrix, the water saturation is ata low, nearly constantflevel. At the face of the matrix and extending for some distance info the block, the water saturation is relatively higher. In the production cycle of such a system, the high water saturation at the face of the fracture would interfere with the production of oil from the interior of the block.

FIGURE 5 illustrates the effect of changing the wettability of the surface of the matrix in this system. At the surface of the matrix, the oil saturation is realtively high. At the interior of the block, beyond the point at which the oil-wetting surfactant has contacted and adhered to the rock surface, the system is water-wet with a relatively low oil saturation and high water saturation. During the production cycle of the system illustrated in FIGURE 5, the initial production will be much higher in oil concentration and consequently much lower in water cut.

DESCRIPTION OF THE PREFERRED EMBODIMENT In a naturally highly fractured reservoir such as the Spraberry Field of West Texas, production wells are drilled. The field is depleted of primary production, additional infll wells are drilled if necessary and waterflooding is initiated. In the preferred embodiment of this invention, a multiple well system is preferred. However,

it is within the scope of this invention to use a single well for both injection' and production.

During the injection phase it is preferred to use all of the wells in the field as injection wells to achieve fiill-up in the shortest time. However it is possible to inject and produce at the same time. It is only essential thatv fluid production be limited to a rate substantially below the water inux thereby raising the reservoir pressure to the desired level. In most instances the maximum reservoir pressure will bev limited to the initial bottom-hole pressure of the reservoir to prevent breakdown of the reservoir confines. However, in certain reservoirs such as the Spraberry, which had an initial bottom-hole pressure of approximately 2 500 p.s.i., the injection bottom-hole pressure may be raised to approximately 3,000 pounds without reservoir damage due to an unusually large shale formation overying the producing horizon,

Water containing approximately 0.5% by weight octadecyl amine acetate is injected continuously unitl the de sired bottom-hole pressure is reached. Although not preferred, this surfactant may be added only-at the latter stage of the injection phase. The octadecyl amine acetate changes the wettability of the rock matrix for adetermina-ble depth into the matrix fromV a water-wet system to an oil-wet system and will concentrate oil near the surface of the matrix block. The depth of penetration of the surfactant into the rock matrix can be readily determined using scale models in the laboratory and conventional techniques well known tothose skilled in the art. v

When the desired bottom-hole pressure is reached and after a sufficient period.of time has elapsed to substantially permit pressure .equilibrium between the fracture system and the porous matrix, the production phase of the cycle is begun. It is preferred to use all wells into the formation as producers in order to obtain the production in the shortest possible time. However, it is within the scope of the invention to continue injection through some wells while liuid is withdrawn through other wells during the production cycle. It is only essential that the fluid production rate be substantially above the water injection rate during the production phase. Production is continued until the produced oil-water ratio reaches an economic limit.

Oil is produced by means of the generated pressure differential between the matrix and fracture system and drawn to the producing wells. Since oil has been concentrated near the surface of the matrix blocks, the amount of oil recovered for a given pressure drop between the fracture and matrix will be substantially increased and the time lapse for a given quantity of oil production will. be reduced.

A second cycle is begun by injection of water without surfactant. Normally surfactant will not need to be added during each injection phase. The benefit of the oil wetting surfactant will be realized for several pressure pulse cycles before the concentration of the surfactant in the matrix is reduced below the acceptable limits. However, once the oil production in the production phase has fallen below acceptable economic limits, additional surfactant can be added 0n later injection phases and the cyclic process continued until the reservoir is depleted.

It is to be understood that while the invention has been explained for purposes of clarity in terms of twophase i.e. an oil-water system, normally three phases of oil, gas and water will be present in the reservoir and that the invention is equally applicable to such a sysem.

What is claimed is:

1. A method for the secondary recovery of oil from a naturally highly fractured reservoir having relatively impermeable matrix blocks and relatively high-permeable fractures and being penetrated by at least one well cornprising:

(a) injecting an aqueous flood medium into the resetu voir to increase the reservoir pressure;

(-b) rendering oil-wet only the exterior portion of at least a portion of the matrix blocks; and

(c) subsequently withdrawing fluid from the reservoir to reduce the reservoir pressure and to recover oil from the reservoir.

2. The method as defined in claim 1 wherein: the matrix blocks are rendered oil-wet by the addition of an oil-wetting surfactant to the injected aqueous flood medium.

3. The method as dened in claim 1 wherein:

(a) the aqueous ood medium is injected through at least one well; and

('b) uid is withdrawn through at least one additional Well.

4. The method as dened in claim 1 wherein the steps of injecting the aqueous flood medium to increase the reservoir pressure and withdrawing uid to decrease the reservoir pressure are cyclically repeated.

5. The method as defined in claim 1 wherein the aqueous flood medium is injected and the uid is withdrawn through the same well. y

6. A method for the secondary `recovery of oil from a naturally highly fractured reservoir having relatively impermeable matrix blocks and relatively highly permeable fractures and penetrated by a plurality of wells compris- (a) injecting an aqueous ood medium into the reservoir through substantially all of the wells;

(b) 4simultaneously injecting a surfactant capable of rendering a portion of the matrix of the reservoir oil-wet, the surfactant'forming a solution with the ood medium and being injected at a rate of approximately 0.5% by weight surfactant in the solution;

(c) ceasing injection and permitting the injected solution to remain in contact with reservoir matrix until References Cited UNITED STATES PATENTS 2,452,736 11/ 1948 Eickrneyer.

2,606,871 8/ 1952 Ten Brink 166--42 X 2,733,206 1/ 1956 Prusick et al.

2,792,894 5/ 1957 Graham et al 166-9 X 2,846,012 8/ 1958 Lorenz et al.

2,908,643 10/ 1959 Thompson et al.

3,219,114 11/1965 Oxford 166-42 3,286,770 11/ 1966 Knox et al 166-9 X 3,368,620 2/1968 Harvey 1669-9 OTHER REFERENCES Enright, R. l.: Spraberry Cyclical Flood May Net 500 Million Bbl. of Oil, in Oil & Gas Jour., Oct. 1, 1962, pp. 68-77.

JAMES A. LEPPINK, Primary Examiner IAN A. CALVERT, Assistant Examiner `U.S. Cl. X.R. 166-275

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Cited By (26)

* Cited by examiner, † Cited by third party
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US4364431A (en) * 1980-12-17 1982-12-21 National Iranian Oil Company Method for recovering oil from an underground formation
US4545620A (en) * 1978-12-15 1985-10-08 Atlantic Richfield Company Process for the recovery of a mineral
FR2631380A1 (en) * 1988-05-11 1989-11-17 Marathon Oil Co Method for oil recovery by using a cyclic change in the wettability
US5014783A (en) * 1988-05-11 1991-05-14 Marathon Oil Company Sequentially flooding an oil-bearing formation with a surfactant and hot aqueous fluid
US5042580A (en) * 1990-07-11 1991-08-27 Mobil Oil Corporation Oil recovery process for use in fractured reservoirs
WO2000023688A1 (en) * 1998-10-19 2000-04-27 Alberta Oil Sands Technology And Research Authority Enhanced oil recovery by altering wettability
US20040157749A1 (en) * 2003-02-11 2004-08-12 Ely John W. Method for reducing permeability restriction near wellbore
US7255166B1 (en) 2004-07-28 2007-08-14 William Weiss Imbibition well stimulation via neural network design
WO2007112199A2 (en) * 2006-03-29 2007-10-04 Geosierra Llc Enhanced hydrocarbon recovery by vaporizing solvents in oil sand formations
US20070251686A1 (en) * 2006-04-27 2007-11-01 Ayca Sivrikoz Systems and methods for producing oil and/or gas
US20080023198A1 (en) * 2006-05-22 2008-01-31 Chia-Fu Hsu Systems and methods for producing oil and/or gas
US20080087425A1 (en) * 2006-08-10 2008-04-17 Chia-Fu Hsu Methods for producing oil and/or gas
US20090056941A1 (en) * 2006-05-22 2009-03-05 Raul Valdez Methods for producing oil and/or gas
US20090155159A1 (en) * 2006-05-16 2009-06-18 Carolus Matthias Anna Maria Mesters Process for the manufacture of carbon disulphide
US20090188669A1 (en) * 2007-10-31 2009-07-30 Steffen Berg Systems and methods for producing oil and/or gas
US20090205823A1 (en) * 2008-02-14 2009-08-20 University Of Houston System Process for enhancing the production of oil from depleted, fractured reservoirs using surfactants and gas pressurization
US20090226358A1 (en) * 2006-05-16 2009-09-10 Shell Oil Company Process for the manufacture of carbon disulphide
US20100108316A1 (en) * 2006-09-08 2010-05-06 Schlumberger Technology Corporation Method of improving recovery from hydrocarbon reservoirs
US20100140139A1 (en) * 2007-02-16 2010-06-10 Zaida Diaz Systems and methods for absorbing gases into a liquid
US20100307759A1 (en) * 2007-11-19 2010-12-09 Steffen Berg Systems and methods for producing oil and/or gas
US20110094750A1 (en) * 2008-04-16 2011-04-28 Claudia Van Den Berg Systems and methods for producing oil and/or gas
US20110108269A1 (en) * 2007-11-19 2011-05-12 Claudia Van Den Berg Systems and methods for producing oil and/or gas
US20110132602A1 (en) * 2008-04-14 2011-06-09 Claudia Van Den Berg Systems and methods for producing oil and/or gas
US8097230B2 (en) 2006-07-07 2012-01-17 Shell Oil Company Process for the manufacture of carbon disulphide and use of a liquid stream comprising carbon disulphide for enhanced oil recovery
US9057257B2 (en) 2007-11-19 2015-06-16 Shell Oil Company Producing oil and/or gas with emulsion comprising miscible solvent
US10053966B2 (en) 2016-05-17 2018-08-21 Nano Gas Technologies Inc. Nanogas flooding of subterranean formations

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Cited By (42)

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Publication number Priority date Publication date Assignee Title
US4545620A (en) * 1978-12-15 1985-10-08 Atlantic Richfield Company Process for the recovery of a mineral
US4364431A (en) * 1980-12-17 1982-12-21 National Iranian Oil Company Method for recovering oil from an underground formation
FR2631380A1 (en) * 1988-05-11 1989-11-17 Marathon Oil Co Method for oil recovery by using a cyclic change in the wettability
US5014783A (en) * 1988-05-11 1991-05-14 Marathon Oil Company Sequentially flooding an oil-bearing formation with a surfactant and hot aqueous fluid
US5042580A (en) * 1990-07-11 1991-08-27 Mobil Oil Corporation Oil recovery process for use in fractured reservoirs
WO2000023688A1 (en) * 1998-10-19 2000-04-27 Alberta Oil Sands Technology And Research Authority Enhanced oil recovery by altering wettability
US6186232B1 (en) 1998-10-19 2001-02-13 Alberta Oil Sands Technology And Research Authority Enhanced oil recovery by altering wettability
US20040157749A1 (en) * 2003-02-11 2004-08-12 Ely John W. Method for reducing permeability restriction near wellbore
US6945327B2 (en) * 2003-02-11 2005-09-20 Ely & Associates, Inc. Method for reducing permeability restriction near wellbore
US7255166B1 (en) 2004-07-28 2007-08-14 William Weiss Imbibition well stimulation via neural network design
WO2007112199A3 (en) * 2006-03-29 2009-02-12 Geosierra Llc Enhanced hydrocarbon recovery by vaporizing solvents in oil sand formations
WO2007112199A2 (en) * 2006-03-29 2007-10-04 Geosierra Llc Enhanced hydrocarbon recovery by vaporizing solvents in oil sand formations
US20090200018A1 (en) * 2006-04-27 2009-08-13 Ayca Sivrikoz Systems and methods for producing oil and/or gas
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